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1-20 of 28
Keywords: methane
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Journal Articles
Publisher: Society of Petroleum Engineers (SPE)
SPE J. 25 (06): 927–934.
Paper Number: SPE-12893-PA
Published: 01 December 1985
... MMP as a function of reservoir temperature, C 7+ molecular weight of the oil, mole percent methane in the injection gas, and the molecular weight of the intermediates (C 2 through C 6 ) in the gas. CO 2 and N 2 are represented in the current correlation by "equivalent" methane/propane- and methane...
Journal Articles
Publisher: Society of Petroleum Engineers (SPE)
SPE J. 23 (03): 501–510.
Paper Number: SPE-10677-PA
Published: 01 June 1983
...Richard C. Nelson Neither pressure alone nor pressurizing with methane affects phase behavior of a particular surfactant/brine/stock-tank-oil system. Oil-recovery efficiency in corefloods is not significantly different whether the stock-tank oil is pressurized with methane or diluted with iso...
Journal Articles
Publisher: Society of Petroleum Engineers (SPE)
SPE J. 23 (02): 365–376.
Paper Number: SPE-10176-PA
Published: 01 April 1983
... production rate drilling fluids and materials mud flow rate dispersion partial pressure ppm upstream oil & gas flow rate drilling mud production chemistry equation sulfide corrosion management oilfield chemistry mole fraction methane petroleum engineer journal drilling fluid management...
Journal Articles
Publisher: Society of Petroleum Engineers (SPE)
SPE J. 22 (02): 219–225.
Paper Number: SPE-9230-PA
Published: 01 April 1982
... for 0 mol% methane. H 2 S effects begin to be more pronounced, however, as the amount of methane in the solvent increases. This appears to indicate that H 2 S is more effective in reducing MMP at higher concentrations of methane. However, when compared on the basis of percentage reduction in MMP...
Journal Articles
Publisher: Society of Petroleum Engineers (SPE)
SPE J. 17 (04): 281–286.
Paper Number: SPE-6098-PA
Published: 01 August 1977
... 8 1977 1 8 1977 1977. Society of Petroleum Engineers drilling fluid management & disposal Upstream Oil & Gas Corrosion Inhibition drilling fluids and materials atm methane Workplace Hazard Production Chemistry Corrosion Management vapor phase solubility sour...
Journal Articles
Publisher: Society of Petroleum Engineers (SPE)
SPE J. 15 (01): 7–12.
Paper Number: SPE-4957-PA
Published: 01 February 1975
...Byron B. Woertz Vapor-liquid equilibrium values (K-values) for nitrogen, CO2, H2S and the paraffin hydrocarbons, methane through n-octane, in methyl cyanoacetate (MCA) were published in 1972. K-values for the hydrocarbons through C4 were based on vapor-liquid equilibrium data obtained using...
Journal Articles
Publisher: Society of Petroleum Engineers (SPE)
SPE J. 13 (03): 147–155.
Paper Number: SPE-3995-PA
Published: 01 June 1973
... for the injected fluid. In this correlation the maximum methane composition is a function of temperature, pressure, and the molecular weights of the C5+ fraction of the oil and the C2+ fraction of the injected fluid. According to Benham, this correlation is conservative in its prediction and should be confirmed...
Journal Articles
Publisher: Society of Petroleum Engineers (SPE)
SPE J. 13 (02): 93–104.
Paper Number: SPE-3476-PA
Published: 01 April 1973
... measured in conventional test cells. On the other hand, earlier results reported by Weinaug and Cordell indicated that vapor-liquid equilibrium relationships of the system methane-n-butane and methane-n-pentane were not affected by the presence of dry sand. Oxford and Huntington studied the revaporization...
Journal Articles
Publisher: Society of Petroleum Engineers (SPE)
SPE J. 12 (04): 283–288.
Paper Number: SPE-3711-PA
Published: 01 August 1972
...Byron B. Woertz A new set of vapor-liquid equilibrium ratios (K-charts) is presented for methane through n-octane, nitrogen, CO 2 and H 2 S, all in methyl cyanoacetate (MCA). The K-values for the hydrocarbons show a temperature inversion at pressures of 1,000 psia and above in that solubility...
Journal Articles
Publisher: Society of Petroleum Engineers (SPE)
SPE J. 12 (01): 21–27.
Paper Number: SPE-3106-PA
Published: 01 February 1972
...) methane-ethane mixtures at temperatures of 100 degrees to 220 degrees F and pressures of 700 to 8,000 psi; (2) methane-propane pressures of 700 to 8,000 psi; (2) methane-propane mixtures and ethane-propane mixtures at 220 degrees F and pressures of 700 to 8,000 psi; and (3) methane-ethane-propane mixtures...
Journal Articles
Publisher: Society of Petroleum Engineers (SPE)
SPE J. 11 (02): 171–175.
Paper Number: SPE-3071-PA
Published: 01 June 1971
...Harley Y. Jennings, Jr.; George H. Newman The interfacial tension of water against mixtures of methane and normal decane bas been measured in the interval 74 to 350 degrees F and 14.7 to 12,000 psia. These measurements show the range of interfacial-tension values obtained with water against...
Journal Articles
Publisher: Society of Petroleum Engineers (SPE)
SPE J. 11 (02): 176–184.
Paper Number: SPE-3100-PA
Published: 01 June 1971
...Byron B. Woertz A set of five methane K-charts has been developed for reservoir-type systems, for pressures above 1,000 psia and temperatures of 0 to 300 degrees F. Convergence psia and temperatures of 0 to 300 degrees F. Convergence pressures used in development of the charts ranged pressures used...
Journal Articles
Publisher: Society of Petroleum Engineers (SPE)
SPE J. 11 (01): 4–6.
Paper Number: SPE-3236-PA
Published: 01 March 1971
... and Matthews and Hurd12 for methane appears in Fig. I. Obviously it is impossible to extrapolate either portion of the curve past the critical point. However, it has been found that a straight line results when the average density of the liquid and vapor is plotted as a function of temperature. Through...
Journal Articles
Publisher: Society of Petroleum Engineers (SPE)
SPE J. 10 (03): 298–310.
Paper Number: SPE-2543-PA
Published: 01 September 1970
... is 1,000 psia or below. At these pressures the methane-LPG transition cannot be pressures the methane-LPG transition cannot be single phase at temperatures below 160 degrees F. The only practicable approach to achieving miscible displacement under these conditions is to inject an ethane-rich buffer slug...
Journal Articles
Publisher: Society of Petroleum Engineers (SPE)
SPE J. 9 (03): 338–342.
Paper Number: SPE-2274-PA
Published: 01 September 1969
... and methylhenzene were used to represent the paraffinic, naphthenic and aromatic components of paraffinic, naphthenic and aromatic components of the heavy fraction. In the mixtures studied, the heavy fraction composition was held constant at 0.05-mole fraction, the balance being methane except for one mixture where...
Journal Articles
Publisher: Society of Petroleum Engineers (SPE)
SPE J. 8 (04): 359–369.
Paper Number: SPE-1848-PA
Published: 01 December 1968
... media porous medium liquid psig Fluid Dynamics sandpack experiment effective permeability enhanced recovery methane viscosity Bernard saturation agent foam quality foam gas saturation liquid saturation permeability The Mechanism of Gas and Liquid Flow Through Porous Media...
Journal Articles
Publisher: Society of Petroleum Engineers (SPE)
SPE J. 8 (03): 281–292.
Paper Number: SPE-2051-PA
Published: 01 September 1968
... Chappelear accuracy Retrograde Condensation shape factor PVT measurement methane calculation composition reference substance experimental data Upstream Oil & Gas liquid phase condensation correlation procedure reservoir fluid A Corresponding States Correlation for Calculating Gas...
Journal Articles
Publisher: Society of Petroleum Engineers (SPE)
SPE J. 8 (02): 157–162.
Paper Number: SPE-1589-PA
Published: 01 June 1968
... in form to van der Waal's equation of state. For the paraffin hydrocarbons methane through n-hexane and nitrogen, an average absolute deviation of 1.9 percent was obtained on 1,006 data points described in the literature by 14 authors. When this equation is extended to complex, liquid hydrocarbon mixtures...
Journal Articles
Publisher: Society of Petroleum Engineers (SPE)
SPE J. 7 (02): 205–220.
Paper Number: SPE-1533-PA
Published: 01 June 1967
... & Simulation displacement process mass transfer Upstream Oil & Gas displacement viscosity convergence pressure hydrocarbon injection enhanced recovery methane finite difference approximation composition enriched gas PVT measurement gradient dispersion equation approximation correlation...
Journal Articles
Publisher: Society of Petroleum Engineers (SPE)
SPE J. 7 (01): 75–79.
Paper Number: SPE-1483-PA
Published: 01 March 1967
...Mario H. Gonzalez; Richard F. Bukacek; Anthony L. Lee Experimental viscosity data for methane are presented for temperatures from 100 to 340F and pressures from 200 to 8,000 psia. A summary is given of the available date for methane, and a comparison is presented for that data common...
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